Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F28—HEAT EXCHANGE IN GENERAL
  • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
  • F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
  • F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
  • F28D20/023—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat the latent heat storage material being enclosed in granular particles or dispersed in a porous, fibrous or cellular structure
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
  • C08K5/00—Use of organic ingredients
  • C08K5/01—Hydrocarbons
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
  • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
  • C08L23/04—Homopolymers or copolymers of ethene
  • C08L23/06—Polyethene
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L2312/00—Crosslinking
  • C08L2312/06—Crosslinking by radiation
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L91/00—Compositions of oils, fats or waxes; Compositions of derivatives thereof
  • C08L91/06—Waxes
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
  • Y02E60/14—Thermal energy storage
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
  • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
  • Y10T428/00—Stock material or miscellaneous articles
  • Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
  • Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]

Definitions

• the present invention relates to a pellet or sheet useful in thermal energy storage and, more particularly, to a pellet or sheet formed from cross- linked polyethylene and having a straight chain crys ⁇ talline alkyl hydrocarbon therein.
• phase change thermal energy storage- systems because of their inherent ability to store and release large quantities of heat to their surrounding environment as tempera ⁇ tures drop below or exceed predetermined levels.
• These systems are of particular interest in the architectural and building trades where climate control and its con ⁇ comitant energy consumption is one of the principal considerations in building design and material selec ⁇ tion.
• phase change materials have been incorporated into concrete such that energv in excess of that necessary to obtain comfort conditions is inherently absorbed and released as required to main- tain the comfort range.
• phase change materials incorporated into the concrete walls or floors of buildings absorb solar energy during daylight hours and release it to the interior at night as temperatures decrease.
• the same phase change materials due to their thermostatic character, conserve coolness by absorbing cool from the night air, and releasing it during the day.
• Concrete materials incorporating phase change materials are more desirable than elements which store only sensible heat because they have a higher capacity to store energy, plus they absorb and release a large quantity of energy over a very narrow temperature range.
• a phase change material utilizes its latent heat of fusion for thermal storage.
• the latent heat of fusion is substantially greater than the sensible heat capacity of the material. Stated differently, the amount of energy which a material absorbs upon melting, or releases upon freezing, is much greater than the amount of energy which it absorbs or releases upon increasing or decreasing in temperature 1°C.
• a phase change material Upon melting and freezing, per unit weight, absorbs and releases substantially more energy than a sensible heat storage material which is heated or cooled to the same temperature range.
• a phase change material absorbs and releases a large quantity of energy in the vicinity of its melting/freezing point.
• the phase change materials also store and release sensible energy as well. Thus, the latent storage in phase change materials is always augmented to a signi- ficant extent by their sensible storage capacity.
• This advantage is put to good use in buildings where space is at a premium and energy storage and release are required within a very narrow comfort range.
• phase change material which could store and release thermal energy within the temperature range of 10-65°C, and could be economically incorporated into concrete, would have broad utility for many heating and cooling applications including solar passive, bridge deck deicing, etc.
• phase change materials have not been achieved because the phase change material adversely affects the physical properties of the concrete.
• Direct incorporation of phase change materials into concrete reduces the strength properties.
• the degree of concrete crosslinking required to achieve optimum physical properties is not obtained in the direct presence of the phase change material.
• U.S. Patent 4,504,402 to Chen teaches an encapsulated phase change material which is prepared by forming a shell about a phase change composition in compacted powder form. These pellets, however, are comparatively expensive to manufacture. Summary of the Invention The present invention is directed to a compo ⁇ site useful in thermal energy storage.
• the composite is formed from crosslinked polyethylene having a straight chain alkyl hydrocarbon incorporated therein as a phase change material.
• the composite is a pellet which is suitable for incorporation into concrete in building materials and the like.
• the composite is a sheet material useful as a wall or floor covering.
• the polyethylene is preferably high density polyethylene, although, low density polyethylenes may also be useful.
• a more particular embodiment of the present invention resides in a pellet useful in thermal energy storage, said pellet being formed from high density or low density- polyethylene and having a straight chain crystalline alkyl hydrocarbon absorbed therein, said polyethylene being crosslinked to such a degree that said pellet maintains its shape (form stability) upon heating and, at the same time, is capable of absorbing at least 10% by weight, and preferably, at least 50% by weight, of said straight chain crystalline alkyl hydrocarbon.
• a thermal storage material comprising a non-polymeric cementitious matrix having pellets containing a phase change material dispersed therein, said pellets being formed from high density or low density polyethylene, said polyethylene being cross ⁇ linked to such a degree that said pellets are form stable and, at the same time, are capable of absorbing at least 10% by weight, and preferably, at least 50% by weight, of said straight chain alkyl hydrocarbon.
• the alkyl hydro ⁇ carbon in the composite is comprised of one or more crystalline straight chain alkyl hydrocarbons having 14 or more carbon atoms and heats of fusion greater than 30 cal/g.
• the melting and freezing point of the alkyl hydrocarbon is in the range of 40-95 ⁇ F, and preferably, 65-75°F.
• the composites of the present invention are useful in thermal energy storage.
• the pellets of the present invention may be formed by the use of commercially available high density or low density polyethylene pellets as the starting component.
• high density polyethy- lene is used herein as it is used in the art, i.e., to refer to polyethylene ranging in density from about 0.940 to about 0.970 g/cc.
• low density polyethylene refers to polyethylenes ranging in density from 0.910 to 0.940 g/cc.
• Representative examples of some of the commercially available high density polyethylene pellets useful in the present invention are Alathon 7040 and Alathon 7050, available from E.I. DuPont; Marlex 6006, available from Phillips Petroleum; LS-556 from U.S. Industrial Chemicals Co.; and. Gulf Oil Co.
• pellets 9606 Lower density polyethylenes form softer, more rubbery composites with the crystal ⁇ line alkyl hydrocarbons that are somewhat less desir ⁇ able due to their lower co pressive strength.
• the pellets used in the present invention may range from about 1 micron to 2.0 mm in their largest dimension, and preferably range from about 0.6 to 1.2 mm. While various shapes may be used, the pellets are typically spherically or cylindricallv shaped, although elongated particles or cubes can also be used.
• the sheets useful as wall or floor coverings in the present invention are typically about 1.5 to 6.0 mm thick.
• the polyethylene pellets and sheets Prior to absorbing the alkyl hydrocarbon, the polyethylene pellets and sheets are crosslinked to impart form stability to them.
• Various methods of crosslinking polyethylene are known. Gamma and elec ⁇ tron beam radiation are the most convenient, and therefore, the preferred methods of crosslinking.
• the electron beam or gamma radiation dose used in the present invention is typically in the range of about 2-12 egarads, and preferably, about 6-10 megarads.
• the amount of irradiation must be adjusted within the aforementioned ranges for the particular pellet or sheet used.
• the irradiation dosage within the above ranges does not appear to have a significant effect on the melting point of the polyethylene, but it clearly affects its capacity to absorb phase change material and its thermal form stability. It is essential that an irradiation dosage be selected which crosslinks the polyethylene sufficiently to render it thermally form stable. If the pellets are not sufficiently cross ⁇ linked, they may partially fuse together or dissolve during the heating process to imbibe the alkyl hydro ⁇ carbon phase change material, or later, upon heating in a thermal energy storage device. At the same time, the pellets and sheets cannot be so heavily crosslinked that they do not absorb the phase change material. In general, in crosslinking the pellet or sheet, a trade-off exists between thermal form stabil ⁇ ity and capacity for phase change material. A radia ⁇ tion dosage should be selected which provides the most desirable balance of these two properties, i.e., thermal form stability with a high capacity for the alkyl hydrocarbon.
• the crosslinked matrix may be examined for thermal form stability by placing a sample of it in refluxing ethylene glycol at 145-165°C and observing it for adhesion.
• the matrix should be form stable, i.e., essentially free of adhesion or tack at tempera ⁇ tures up to about 150°C.
• Alathon 7040 pellets When Alathon 7040 pellets receive a total dosage of 2-4 megarads, they fuse into a single mass within 2.5 hours at 145 to 165°C and are not suitable as a thermal energy storage medium. At 6 megarads, they may adhere together after 72 hours, but the mass is easily crumbled and the pellets are useful as a phase change material. With exposures of 8 megarads or more, the pellets remain free flowing. Similar results are obtained with Marlex 6006 pellets although pellets receiving 8 megarads exposure adhere at their points of contact after 3 hours at 165°C in refluxing ethylene glycol. USI LS-630 pellets require 10-12 megarad dosages before they are sufficiently thermal form stable to be useful as a storage medium.
• the crosslinked, high density polyethylene matrix forming the composites of the present invention can also be characterized by a gel content of at least 10%, and more preferably, at least 30%. Resistance to melt flow or thermal flow stability is related to the gel content of the crosslinked material. The final gel content varies with the high density polyethylene used; depending on the product, gel contents of 30-50% and up to 90% may be achieved. The capacity of the pellets and sheets to absorb the phase change material is equally as impor ⁇ tant as their form stability and must also be consi ⁇ dered in selecting the optimum radiation dosage.
• these materials may be crosslinked to a state in which they are form stable, but they are not desir ⁇ able for thermal energy storage due to their low capacity for the phase change material.
• the degree of crosslinking is controlled such that the pellet or sheet is capable of absorbing at least 10% by weight phase change material, and preferably, at least 50% by weight.
• the desired irradiation dosage can be achieved with various combinations of electron beam voltage and beam current, it has been found that these conditions should be in the ranges of greater than about 500,000 volts and about 3-33 milliamps to uniformly crosslink the pellets or sheets and achieve the desired thermal form stability and capacity for phase change material.
• the maximum beam potential available is typically 3-5 million volts. If the poten ⁇ tial is in excess of 10 million volts, residual radia- tion becomes a factor.
• the beam potentials useful in the present invention range from about 500,000 to 10 million volts.
• Radiation dose can be expressed by the equa ⁇ tion:
• Fi and Fe are the beam current and beam energy efficiencies
• I is the beam current
• V is the beam potential
• t is the bed depth in g/cm
• A/T is the area thruput in cm /hr.
• the maximum permissible pellet bed depth is about 0.30 cm. At potentials nearing 5 million volts, the bed depth can be up to 1.25 cm. At these voltages and bed depths, equal entrance and exit energy is achieved and the pellets are uniformly penetrated by the electron beam. Similar voltages can be used to process sheets. While it is not necessarily essential to have uniform crosslinking, it is generally desirable. Non-uniformly crosslinked pellets, for example, pellets having a higher degree of crosslinking in the shell than the core, are useful in many applications.
• the velocity with which a pellet bed or an extruded sheet can be passed through the electron beam is a function of the beam current.
• crosslinking pellets by adjusting the bed . depth for the beam potential, equal entrance and exit energies are achieved and it is unnecessary to agitate the pellet bed to achieve uniform crosslinking. Such agitation may be desirable if higher bed depths are used and processed by multiple passes. In such cases, the bed may be agitated by stirring between passes. This technique may be used when processing large quantities although it is preferable to limit the bed depths as above such that irradiation can be conducted in one pass without agitation. Irradiation in an oxygen containing atmos ⁇ phere, such as air, is accompanied by the production of ozone which can lead to some surface oxidation.
• a typical example of the irradiation condi ⁇ tions used to crosslink Alathon 7040 pellets is:
• Pellets and sheets can also be easily cross ⁇ linked through gamma radiation. Dosages in the range of about 4 to 12 megarads may be used. Irradiation is preferably carried out in an inert atmosphere such as ' nitrogen, helium, hydrogen or a vacuum. It may also be carried out in air, but requires significantly higher total doses than in an inert atmosphere. A nitrogen atmosphere is the lowest cost and therefore, the preferred irradiation atmosphere. Chemical crosslinking is also feasible. U.S.
• silane-grafted method high density polyethylene is charged to a Banbury with vinyl triethoxy silane containing benzoyl peroxide and mixed with steam. These silane-grafted high density polyethylene pieces are then coextruded with a catalyst and crosslinked by heating in boiling water and then air dried.
• high density polyethy ⁇ lene powder may be dry blended with dicumyl peroxide, di-t-butyl peroxide, or a similar high temperature free radical generating agent and melt extruded at about 150 to 200°C, and preferably, about 175°C, to crosslink the polyethylene.
• HDPE powder is melted on a mill, and as soon as a smooth sheet of polyethylene is formed, dicumyl peroxide may be added.
• Dicumyl perox ⁇ ide is usually reacted in an amount of about 0.1 to 5% by weight, and preferably, about 1% by weight.
• crosslinked sheets which can be used in the manufacture of floor or wall coverings or which can be cut into pellets.
• the crosslinked pellets or sheets are then impregnated with an alkyl hydrocarbon to obtain products in accor ⁇ dance with the present invention.
• Processes such as compression or injection molding can also be used to form the pellets, but they tend to be less economical. They are however, useful in forming floor or wall coverings.
• sheets, tiles, or the like are formed by compression or injection molding and crosslinked simultaneously or afterward by electron beam or gamma radiation as described above.
• the straight chain alkyl hydrocarbon is perferably incorporated into the crosslinked HDPE pellet or sheet by immersing the pellets or sheets into a bath of melted straight chain alkyl hydrocar ⁇ bons. The pellets or sheets are retained in the bath until at least about 10% by weight of the straight chain alkyl hydrocarbon is absorbed. Absorption of about 40 to 80% by weight of the alkyl hydrocarbon is preferred in the case of the pellets.
• the time/ temperature required to achieve this capacity of phase change material will depend on the degree of cross- linking. This degree of absorption is achieved by allowing pellets to remain in a wax melt for about 1 to 2 hours at about 150 to 175°C.
• a number of commercially available waxes are useful as phase change materials in the present inven- tion including Shellwax 100 (MP 42-44°C) , Shellwax 120 (MP 44-47°C) , Shellwax 200 (MP 52-55°C) , Shellwax 300 (MP 60-65°C) , Boron R-152 (MP 65°C) , Union SR-143 (MP about 61°C) , Witco 128 (MP about 53°C) Witco LLN, Witco 45A, Witco K-61, Witco K-51, and Witco 85010-1, Aristowax 143 (MP 34-61°C) , and Paraffin 150 (MP about 61°C) .
• These waxes have heats of fusion greater than 30 cal/g and by comparison to other phase change materials, they are inexpensive. Many of them cost as little as 15jzf (U.S.) per pound when purchased in a tank car quantity.
• a preferred group of waxes for use in the present invention are mixtures of crystalline alkyl hydrocarbons which melt in the range of 10 to 50 ⁇ C. Mixtures of alkyl hydrocarbons are obtained at low cost as by-products of petroleum refining. Because they are inexpensive, they can be incorporated into building materials at minimal additional expense and, at the same time, provide high savings in terms of reduced energy costs.
• the preferred blends for pas ⁇ sive heating have a melting and freezing point in the range of 24 to 33°C.
• Preferred blends for passive cool storage have a melting and a freezing point in the range of 18 to 33 C C.
• the blends will be relied upon for both heating and cool ⁇ ing and will be characterized by both the melting and a freezing point in the range of 20 to 25 ⁇ C.
• ultra pure alkyl hydrocarbons C-16 to C-22 and higher are also available at a premium cost that may have higher heats of fusion and crystallization (e.g., 55-60 cal/g) than the low-cost mixtures de ⁇ scribed above. These ultra pure alkyl hydrocarbons are also useful in the present invention for critical applications requiring maximum storage capacity in the minimum volume of space.
• the difference between the melting and freezing points is Another important consideration in the selec ⁇ tion of waxes used in the present invention.
• the alkyl hydrocarbons are self-nucleating and thus melt and freeze congruently. Thus, when heated or cooled at rates of l°C/min. or less, the melting and freezing temperatures coincide. However, it is desir ⁇ able to have phase change materials that show little or no super cooling even when cooled at rapid rates such as 10°C/min. as in a differential scanning calor ⁇ imeter test.
• the difference between the melting and freezing points of the wax should be less than 10°C to avoid supercooling. Preferably, this difference is less than 5°C, and more preferably, less than about 3°C, and in many cases, the melting and freezing points are the same.
• phase change materials which exhibit phase change characteristics which are intermediate or approximately the average of the individual phase change materials making up the blend
• polyethylene three phase changes are observed, those of the two or more waxes, plus that of the polyethy- lene.
• Such a blend is useful in applications where the phase change material is relied upon to conserve heat in the winter and conserve cool in the summer.
• the difference in the melting points of the phase change materials should be at least 50°C.
• waxes as commercially obtained, are not preferred for use in passive energy storage systems as used in climate control, because they melt over a broad range, or their melting points are too high. Consequently, in accordance with the invention, these materials may be combined with crystalline alkyl hydrocarbons having 14-34 carbon atoms and, more specifically, 16 or 28 carbon atoms, in order to bring the melting point of the blend within the range of 16-42°C.
• crys- talline-to-amorphous phase change of the high density polyethylene is preserved in the composite sheets or pellets, with however, the melting point of the HDPE lowered from 132°C to about 115°C.
• Another embodiment of the present invention utilizes flame-resistant halogenated hydrocarbons as fire-retardant additives to the alkyl hydrocarbon phase change materials.
• Typical examples of flame- resistant hydrocarbons are halogenated hydrocarbons, such as chlorinated or fluorinated hydrocarbons. Representative examples include Chlorowax 70, avail- able from Diamond Shamrock and decabromodiphenylether, available from Ethyl Corp. These halogenated fire- retardants can be used ih admixture with conventional flame-resistant fillers such as antimony oxide or a blend of pentaerythritol and onoammonium phosphate, etc.
• the weight ratio of halogenated fire-retardant- to-filler may vary, but it is typically about 1:1 to 3:1.
• Flame-resistant halogenated fire-retardant formulations have previously been added to polymers to render them self-extinguishing. Some of the fire- retardant materials used for this purpose may also be useful as flame-resistant phase change materials by themselves in accordance with the present invention.
• the cementitious composition of the present invention includes a cementitious material as a rigid matrix forming material. Typical examples of useful cementitious materials are hydraulic cements, gypsum, plaster of Paris, lime, etc. Portland cement is by far the most widely used hydraulic cement. Portland cements are ordinarily used for construction purposes. Types I, II, III, IV, and V may be used. White ce ⁇ ments, air entrained cements, high alumina cements, and masonry cements may also be used.
• Concretes are mixtures of hydraulic cements and aggregates.
• Typical aggregates include conven ⁇ tional coarse aggregates, such as gravel, granite, limestone, quartz sieve, etc., as well as so-called fine aggregates, such as sand and fly ash.
• Conven ⁇ tional hydraulic cement concretes for example, Port ⁇ land cement concretes, employ major amounts, about 50-70% by volume of such aggregates in the set product. These cements and concretes fall within the term "cementitious material" as it is used herein.
• the cementitious compositions of the present invention also include concrete and plaster composi ⁇ tions useful in the manufacture of pre-formed materi ⁇ als, such as concrete blocks, dry wall, and the like, as well as in forming poured concrete structures such as used in forming the walls, floors, floor pads, and partitions of buildings.
• the composi ⁇ tions of the present invention also include composi ⁇ tions useful in roadway, runway, and bridge deck construction where icing may be prevented by incorpor ⁇ ation of the phase change material for thermal energy storage during the day, and release during the night to prevent freezing of the water on the surface.
• the pellets of the present invention can also be incorpor ⁇ ated into bricks, including unfired clay bricks.
• the cementitious compositions of the present invention can be designed for use in various passive thermal storage applications by appropriately select ⁇ ing the melting point of the alkyl hydrocarbons.
• Alkyl hydrocarbons which melt in the range of about 20-42°C are used in passive solar heating, such as in building materials and the structures previously mentioned.
• alkyl hydrocarbons which melt at about 5-15°C are preferably used.
• a partial listing of building materials which may be modified to incorporate alkyl hydrocarbons as phase change materials in accordance with the present invention includes: concrete block, concrete brick, concrete slab, dry wall, and gypsum board.
• the amount of alkyl hydrocarbon-containing pellet used in the cementitious or concrete materials is typically about 5 to 25% by weight. The amount will vary with the density of the concrete used. At least 5 weight percent is required for adequate storage capacity. In excess of 25% by weight pellet, usually reduces the strength characteristics of a product to a level at which it is less useful.

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• 1985
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